US910858A - Production of hydrazin. - Google Patents

Production of hydrazin. Download PDF

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Publication number
US910858A
US910858A US40000207A US1907400002A US910858A US 910858 A US910858 A US 910858A US 40000207 A US40000207 A US 40000207A US 1907400002 A US1907400002 A US 1907400002A US 910858 A US910858 A US 910858A
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hydrazin
ammonia
monochloramin
excess
production
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US40000207A
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Friedrich Raschig
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B21/00Nitrogen; Compounds thereof
    • C01B21/082Compounds containing nitrogen and non-metals and optionally metals
    • C01B21/16Hydrazine; Salts thereof

Definitions

  • the first reaction resulting in the production of hydrazin is favored and yields up to from 70 to 80% of the theoretical amount of hydrazin can be obtained.
  • the addition of formaldehyde solution also influences favorably the production of hydrazin, in all robability because of the formation of carbohydrates by the reaction on the formaldehyde of alkali formed during the production of the monochloramin. In all cases an excess of ammonia tends to increase the yield of hydrazin.
  • Example 1 Add one (1) liter of sodium hypochlorite solution containing about seventy (70) grams ofactivech lorin to one (1) liter of twenty (20) per cent. ammonia's olution, the temperature being preferably ke t below fifteen (15) degrees centigrade. T e formation of the monochloramin takes place very rapidly and the mixture obtained con-' tains no trace of hypochlorite, but only chloramin and an excess of ammonia. The mixture should without delay be heated to the boiling ⁇ point, whereupon a reaction according to t e equation takes place side by side with the formation of nitrogen.
  • Hydrazin is formed and can easily be isolated in the form of the very difficultly soluble sulfate by boiling away the excess of ammonia, acidifying with sulfuric acid, and evaporating till crystallization commences. From twenty-five (25), to thirty (30), grams of hydrazin sulfate, that is, from twenty (20), to t'wenty-five( 25), per cent. of the theoretical yield, are obtained.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

UNITED STATES PATENT OFFICE.
FRIEDRICH RASOHIG, OF LUDWIGSHAFEN-ON-THE-RHINE, GERMANY,
PRODUCTION OF HYDRAZIN.
Specification of Letters Patent.
Patented If an. v26, 1909,
Application filed October 31, 1907. Serial No. 400,002.
To all whom it may concern:
Be it known that I, FRIEDRICH RAsoHIG, doctor of philosophy and chemist, subject of the King of Bavaria, residing at Ludwigshafen on the Rhine, Germany, have invented new and useful Improvements in the.
' suggested that during this reaction a prodnot, monochloramin NH Cl, containing one molecule less water, is formed (Proc. Chem. Soc. 1890, p. 24). It can easily -be proved that this suggestion is correct, for a solution of sodium hypochlorite to which ammonia has been added no longer shows the general reaction of hypochlorites of imparting a violet coloration to anilin-water. It therefore no longer contains hypochlorous acid and actually by distillation in cacao a compound of the composition NH Cl can be isolated in the form of a very volatile oil which is easily soluble in water and possesses a disagreeable odor of chlorid of nitrogen.
I have now discovered that monochloramin can by treatment with ammonia be made to form hydrazin according to the equation NH,01+ NH, NHZNHZIICI.
In order to pre are hydrazin with advantage according to t 's reaction, it is unnecessary and, indeed, inadvisable to isolate the extremely decomposable and oisonou s r nonochloramin and subsequent y treat it with ammonia, but I prefer to treat a hypochlorite directly with an excess of ammonia. The formation of monochloramin takes place practically at once and subsequently two reactions tend to take place of which the first is re resented by the equation given above and feads to the formation of hydrazin, while the second reaction leads to the formation of ammonium chlorid and the liberation of free nitrogen according to the equation Ihave discovered that the second and-undesirable reaction tends to preponderate 1f the mixture of the monochloramin with excess of ammonia be allowed to stand in the cold, or if a catalyser such for instance as small quantities of iron and copper, or a compound such as acetone which lowers-the viscosity of the solution be present. On the other hand, if the mixture containing the monochloramin and ammonia is heated without delay, preferably to the boiling point, or if, either When hot, or when cold, a com ound which increases the viscosity, of the so ution such for instance, as glycerin, sugar, starch, casein, albumen, gum, and glue, is present, the first reaction resulting in the production of hydrazin is favored and yields up to from 70 to 80% of the theoretical amount of hydrazin can be obtained. The addition of formaldehyde solution also influences favorably the production of hydrazin, in all robability because of the formation of carbohydrates by the reaction on the formaldehyde of alkali formed during the production of the monochloramin. In all cases an excess of ammonia tends to increase the yield of hydrazin.
The following examples will serve to illustrate further the nature of my invention and the method'of carrying it into practical effect, but my invention is not confined to these examples.
Example 1. Add one (1) liter of sodium hypochlorite solution containing about seventy (70) grams ofactivech lorin to one (1) liter of twenty (20) per cent. ammonia's olution, the temperature being preferably ke t below fifteen (15) degrees centigrade. T e formation of the monochloramin takes place very rapidly and the mixture obtained con-' tains no trace of hypochlorite, but only chloramin and an excess of ammonia. The mixture should without delay be heated to the boiling }point, whereupon a reaction according to t e equation takes place side by side with the formation of nitrogen. Hydrazin is formed and can easily be isolated in the form of the very difficultly soluble sulfate by boiling away the excess of ammonia, acidifying with sulfuric acid, and evaporating till crystallization commences. From twenty-five (25), to thirty (30), grams of hydrazin sulfate, that is, from twenty (20), to t'wenty-five( 25), per cent. of the theoretical yield, are obtained.
- the boiling Example 2. Stir together three hundred (300) grams of bleaching powder with one (1) liter of twenty (20) per cent. ammonia solution and then rapidly heat the mixture to oint, whereupon considerable quantities o hydrazin are formed. In this case also it can be isolated in the form of hydrazin sulfate by'boiling off the excess of ammonia, acidifying with sulfuric acid, filtering ofl the calcium sulfate formed and evaporatin till crystallization commences.
xample 3; Add twelve (12) cubic centimeters of a five (5) per cent. glue solution to three (3) liters of twenty (20) per cent. ammonia solution, then add further one (1) liter of sodium hypochlorite solution containing about seventy (70) grams of active chlorin, 'and then heat up the mixture finally driving off the excess of ammonia. The residue contains hydrazin which can be conveniently isolated by evaporating the residue and precipitating the hydrazin in the form of its sulfate.
Now what I claim is:
1. The process of producinghydrazin by reacting on monochloramin with ammonia.
2. The process of producing hydrazin by heating monochloramin with an excess of ammonia.
3. The process of producing hydrazin by reacting on monochloramin with ammonia in the presence of a com ound which increases the Viscosity of the so ution.
4. The process of producing hydrazin by reacting on monochloramin with ammonia in the presence of glue.
5. The process of producing hydrazin by heating monochloramin with an excess'of ammonia in the presence of glue.
In testimony whereof I have hereunto set my hand 1n the presence of two subscribing witnesses.
FRIEDRICH RASCHIG. Witnesses:
ERNEST F. EHRHARDT, Jos. H. LEUTE.
US40000207A 1907-10-31 1907-10-31 Production of hydrazin. Expired - Lifetime US910858A (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2675301A (en) * 1950-10-23 1954-04-13 Kellogg M W Co Production of hydrazine
US2698286A (en) * 1949-05-31 1954-12-28 Battelle Development Corp Dehydration of hydrazine solutions
US2710248A (en) * 1950-01-17 1955-06-07 Univ Ohio State Res Found Process of forming hydrazine
US2784057A (en) * 1952-10-15 1957-03-05 Exxon Research Engineering Co Process for treating spent hypochlorite solutions
US2785052A (en) * 1951-06-22 1957-03-12 Metalectro Corp Production of hydrazine
US2837409A (en) * 1954-03-10 1958-06-03 Univ Ohio State Res Found Chloramine process
US2863728A (en) * 1955-10-17 1958-12-09 Univ Ohio State Res Found Production of hydrazine
US2917369A (en) * 1951-06-22 1959-12-15 Nat Distillers Chem Corp Production of hydrazine
US3034861A (en) * 1959-06-26 1962-05-15 John A Pursley Process for preparing hydrazine
JP2020513385A (en) * 2016-11-22 2020-05-14 シェフラー テクノロジーズ アー・ゲー ウント コー. カー・ゲーSchaeffler Technologies AG & Co. KG Method for storing energy in the form of hydrazine carbonate

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2698286A (en) * 1949-05-31 1954-12-28 Battelle Development Corp Dehydration of hydrazine solutions
US2710248A (en) * 1950-01-17 1955-06-07 Univ Ohio State Res Found Process of forming hydrazine
US2675301A (en) * 1950-10-23 1954-04-13 Kellogg M W Co Production of hydrazine
US2785052A (en) * 1951-06-22 1957-03-12 Metalectro Corp Production of hydrazine
US2917369A (en) * 1951-06-22 1959-12-15 Nat Distillers Chem Corp Production of hydrazine
US2784057A (en) * 1952-10-15 1957-03-05 Exxon Research Engineering Co Process for treating spent hypochlorite solutions
US2837409A (en) * 1954-03-10 1958-06-03 Univ Ohio State Res Found Chloramine process
US2863728A (en) * 1955-10-17 1958-12-09 Univ Ohio State Res Found Production of hydrazine
US3034861A (en) * 1959-06-26 1962-05-15 John A Pursley Process for preparing hydrazine
JP2020513385A (en) * 2016-11-22 2020-05-14 シェフラー テクノロジーズ アー・ゲー ウント コー. カー・ゲーSchaeffler Technologies AG & Co. KG Method for storing energy in the form of hydrazine carbonate

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